Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Modelica_3.2.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.2.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2")
translateModel(Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.2.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001216/0.001216, allocations: 108 kB / 16.42 MB, free: 6.469 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001223/0.001223, allocations: 190 kB / 17.36 MB, free: 5.707 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.269/1.269, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.49e-05/1.49e-05, allocations: 2.281 kB / 327.2 MB, free: 3.336 MB / 270.1 MB
Notification: Performance of NFInst.instantiate(Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2): time 0.03134/0.03136, allocations: 36.77 MB / 364 MB, free: 14.43 MB / 318.1 MB
Notification: Performance of NFInst.instExpressions: time 0.176/0.2074, allocations: 15.13 MB / 379.1 MB, free: 9.785 MB / 318.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.002473/0.21, allocations: 47.72 kB / 379.1 MB, free: 9.785 MB / 318.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.001651/0.2116, allocations: 0.6899 MB / 379.8 MB, free: 9.785 MB / 318.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.006639/0.2183, allocations: 2.515 MB / 382.3 MB, free: 9.734 MB / 318.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.009349/0.2276, allocations: 3.764 MB / 386.1 MB, free: 9.621 MB / 318.1 MB
Notification: Performance of NFFlatten.flatten: time 0.007662/0.2353, allocations: 4.905 MB / 391 MB, free: 9.551 MB / 318.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.001982/0.2373, allocations: 1.249 MB / 392.3 MB, free: 9.434 MB / 318.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.003563/0.2409, allocations: 1.968 MB / 394.2 MB, free: 9.363 MB / 318.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.001953/0.2428, allocations: 1.664 MB / 395.9 MB, free: 9.168 MB / 318.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0002398/0.2431, allocations: 162.7 kB / 396 MB, free: 9.168 MB / 318.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.004635/0.2477, allocations: 2.428 MB / 398.5 MB, free: 9.141 MB / 318.1 MB
Notification: Performance of combineBinaries: time 0.002/0.2497, allocations: 3.433 MB / 401.9 MB, free: 7.691 MB / 318.1 MB
Notification: Performance of replaceArrayConstructors: time 0.001016/0.2508, allocations: 2.056 MB / 404 MB, free: 6.457 MB / 318.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0004135/0.2512, allocations: 287.2 kB / 404.2 MB, free: 6.402 MB / 318.1 MB
Notification: Performance of FrontEnd: time 0.0002271/0.2514, allocations: 45.5 kB / 404.3 MB, free: 6.391 MB / 318.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 315 (247)
 * Number of variables: 327 (249)
Notification: Performance of Bindings: time 0.00629/0.2577, allocations: 8.95 MB / 413.2 MB, free: 1.719 MB / 318.1 MB
Notification: Performance of FunctionAlias: time 0.0009052/0.2586, allocations: 1.255 MB / 414.5 MB, free: 0.5977 MB / 318.1 MB
Notification: Performance of Early Inline: time 0.005101/0.2638, allocations: 5.412 MB / 419.9 MB, free: 11.23 MB / 334.1 MB
Notification: Performance of simplify1: time 0.0004223/0.2642, allocations: 369.3 kB / 420.3 MB, free: 10.89 MB / 334.1 MB
Notification: Performance of Alias: time 0.00477/0.269, allocations: 4.434 MB / 424.7 MB, free: 6.164 MB / 334.1 MB
Notification: Performance of simplify2: time 0.0003732/0.2693, allocations: 334.2 kB / 425 MB, free: 5.852 MB / 334.1 MB
Notification: Performance of Events: time 0.00149/0.2708, allocations: 1.425 MB / 426.5 MB, free: 4.398 MB / 334.1 MB
Notification: Performance of Detect States: time 0.001317/0.2722, allocations: 1.339 MB / 427.8 MB, free: 3.062 MB / 334.1 MB
Notification: Performance of Partitioning: time 0.001978/0.2742, allocations: 1.843 MB / 429.6 MB, free: 1.047 MB / 334.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (252/351)
****************************
(1)       [DISC] (1) Boolean $SEV_29
(2)       [DISC] (1) Boolean $SEV_28
(3)       [DISC] (1) Boolean $SEV_27
(4)       [DISC] (1) Boolean $SEV_26
(5)       [ALGB] (1) Real[1] pipe2.flowModel.rhos_act (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {1.0 for $i1 in 1:1})
(6)       [DISC] (1) Boolean $SEV_25
(7)       [DISC] (1) Boolean $SEV_24
(8)       [ALGB] (2) protected Real[2] tank3.portsData_height2
(9)       [DISC] (1) Boolean $SEV_20
(10)      [ALGB] (1) Real valveDiscrete.port_b_T = Modelica.Fluid.Utilities.regStep(-995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.temperature(valveDiscrete.state_b), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.temperature(Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.setState_phX(valveDiscrete.port_b.p, valveDiscrete.port_b.h_outflow, {})), valveDiscrete.m_flow_small) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(11)      [ALGB] (1) Real pipe2.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(12)      [DISC] (1) Boolean $TEV_2
(13)      [ALGB] (1) Real[1] tank2.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(14)      [DISC] (1) Boolean $TEV_1
(15)      [DISC] (1) Boolean $TEV_0
(16)      [ALGB] (3) Real[3] tank2.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1000.0 for $i1 in 1:3})
(17)      [ALGB] (1) Real tank3.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(18)      [ALGB] (1) Real[1] pipe2.flowModel.Fs_p
(19)      [ALGB] (1) protected Real valveDiscrete.state_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(20)      [ALGB] (1) Real[1] pipe3.flowModel.Res_turbulent_internal = pipe3.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(21)      [ALGB] (2) Real[2] pipe1.flowModel.mus = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.flowModel.Medium.dynamicViscosity(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(22)      [ALGB] (2) Real[2] pipe3.flowModel.mus = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.flowModel.Medium.dynamicViscosity(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(23)      [DISC] (1) Boolean $SEV_19
(24)      [DISC] (2) Boolean[2] $SEV_36[$i1]
(25)      [DISC] (1) Boolean $SEV_18
(26)      [ALGB] (2) final Real[2] pipe2.flowModel.roughnesses = {pipe2.roughness, pipe2.roughness} (min = {0.0 for $i1 in 1:2})
(27)      [ALGB] (1) Real[1] pipe3.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(28)      [DISC] (1) Boolean $SEV_17
(29)      [ALGB] (2) protected Real[2] tank3.portsData_diameter2
(30)      [DISC] (1) Boolean $SEV_16
(31)      [ALGB] (3) protected Real[3] tank2.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:3})
(32)      [ALGB] (3) protected Real[3] tank2.levelAbovePort
(33)      [ALGB] (1) Real tank2.level (start = tank2.level_start, StateSelect = prefer)
(34)      [DISC] (3) Boolean[3] $SEV_14[$i1]
(35)      [ALGB] (1) protected Real[1] tank1.portsData_diameter2
(36)      [ALGB] (1) Real[1] pipe3.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(37)      [ALGB] (1) Real[1] tank1.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank1.crossArea) * 2.0 * tank1.level + tank1.crossArea}
(38)      [ALGB] (2) Real[2] pipe2.flowModel.rhos = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.flowModel.Medium.density(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(39)      [ALGB] (1) Real pipe3.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(40)      [ALGB] (1) stream Real[1] tank1.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(41)      [ALGB] (1) Real[1] pipe3.flowModel.Ib_flows
(42)      [ALGB] (1) Real[1] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths
(43)      [ALGB] (1) final input Real[1, 1] tank1.heatTransfer.states.p = {tank1.medium.state.p} (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(44)      [ALGB] (1) Real tank3.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(45)      [ALGB] (1) final Real tank3.fluidVolume = tank3.fluidVolume
(46)      [ALGB] (1) Real tank2.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(47)      [DISC] (1) protected Boolean[1] tank1.aboveLevel
(48)      [ALGB] (1) protected Real valveDiscrete.state_b.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(49)      [ALGB] (3) protected Real[3] tank2.portsData_diameter2
(50)      [ALGB] (1) Real tank2.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank2.medium.T_degC))
(51)      [ALGB] (1) Real tank1.mb_flow
(52)      [ALGB] (2) protected Real[2] tank3.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:2})
(53)      [DISC] (3) Boolean[3] $SEV_0[$i1]
(54)      [ALGB] (1) Real[1] pipe1.flowModel.rhos_act (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {1.0 for $i1 in 1:1})
(55)      [ALGB] (1) Real tank3.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank3.medium.T_degC))
(56)      [ALGB] (1) Real tank1.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank1.medium.T_degC))
(57)      [ALGB] (1) flow Real[1] tank3.heatTransfer.heatPorts.Q_flow
(58)      [ALGB] (2) final Real[2] pipe3.flowModel.dimensions = {(4.0 * pipe3.crossArea) / pipe3.perimeter, (4.0 * pipe3.crossArea) / pipe3.perimeter}
(59)      [ALGB] (4) input Real[2, 2] pipe3.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {1.0 for $i1 in 1:2}, max = {1e4 for $i1 in 1:2}, nominal = {300.0 for $i1 in 1:2})
(60)      [ALGB] (1) flow Real[1] tank3.topPorts.m_flow (start = {0.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(61)      [ALGB] (1) final input Real[1, 1] tank2.heatTransfer.states.T = {tank2.medium.state.T} (start = {288.15 for $i1 in 1:1}, min = {1.0 for $i1 in 1:1}, max = {1e4 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(62)      [ALGB] (1) flow Real[1] tank2.heatTransfer.heatPorts.Q_flow
(63)      [ALGB] (1) Real[1] tank1.ports.p (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(64)      [ALGB] (1) stream Real pipe1.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(65)      [ALGB] (3) protected Real[3] tank2.bottomArea
(66)      [ALGB] (1) Real[1] pipe1.flowModel.Fs_fg
(67)      [ALGB] (1) final input Real[1, 1] tank1.heatTransfer.states.T = {tank1.medium.state.T} (start = {288.15 for $i1 in 1:1}, min = {1.0 for $i1 in 1:1}, max = {1e4 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(68)      [ALGB] (1) Real[1] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(69)      [ALGB] (1) Real $FUN_9
(70)      [ALGB] (1) final Real tank1.fluidVolume = tank1.fluidVolume
(71)      [ALGB] (1) Real $FUN_8
(72)      [ALGB] (1) Real tank2.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(73)      [ALGB] (1) Real[1] pipe2.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(74)      [ALGB] (1) Real $FUN_7
(75)      [ALGB] (1) Real $FUN_6
(76)      [ALGB] (1) Real[1] pipe1.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(77)      [ALGB] (1) Real $FUN_4
(78)      [ALGB] (1) protected Real valveDiscrete.state_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(79)      [ALGB] (1) Real $FUN_3
(80)      [ALGB] (3) protected Real[3] tank2.portsData_diameter = tank2.portsData.diameter
(81)      [ALGB] (1) Real $FUN_2
(82)      [DISC] (2) Boolean[2] $SEV_35[$i1]
(83)      [ALGB] (1) Real[1] tank1.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(84)      [ALGB] (1) Real tank3.level (start = tank3.level_start, StateSelect = prefer)
(85)      [ALGB] (1) Real $FUN_1
(86)      [ALGB] (1) Real[1] pipe2.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(87)      [ALGB] (1) final Real[1] pipe1.flowModel.dheights = {pipe1.height_ab}
(88)      [ALGB] (1) stream Real pipe1.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(89)      [ALGB] (1) Real[1] pipe1.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(90)      [ALGB] (2) protected Real[2] tank3.portsData_diameter = tank3.portsData.diameter
(91)      [ALGB] (1) Real $FUN_21
(92)      [ALGB] (1) Real tank2.mb_flow
(93)      [ALGB] (1) Real $FUN_20
(94)      [ALGB] (2) Real[2] pipe2.flowModel.mus = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.flowModel.Medium.dynamicViscosity(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(95)      [DISC] (3) Boolean[3] $SEV_13[$i1]
(96)      [ALGB] (4) input Real[2, 2] pipe3.flowModel.states.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(97)      [DISC] (3) Boolean[3] $SEV_9[$i1]
(98)      [ALGB] (1) final input Real[1, 1] tank2.heatTransfer.states.p = {tank2.medium.state.p} (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(99)      [ALGB] (1) Real[1] pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths
(100)     [ALGB] (1) Real[1] tank2.heatTransfer.Q_flows
(101)     [ALGB] (1) Real valveDiscrete.dp (start = valveDiscrete.dp_start)
(102)     [DER-] (1) Real $DER.tank1.U
(103)     [ALGB] (1) Real[1] pipe2.flowModel.Ib_flows
(104)     [ALGB] (1) Real[1] pipe3.flowModel.dps_fg (start = {pipe3.flowModel.p_a_start - pipe3.flowModel.p_b_start for $i1 in 1:1})
(105)     [ALGB] (3) Real[3] tank2.ports.p (start = {1e5 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e5 for $i1 in 1:3})
(106)     [ALGB] (3) stream Real[3] tank2.ports.h_outflow (min = {-1e10 for $i1 in 1:3}, max = {1e10 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3})
(107)     [ALGB] (1) Real tank1.Hb_flow
(108)     [ALGB] (1) Real pipe3.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(109)     [ALGB] (3) protected Real[3] tank2.portsData_height2
(110)     [ALGB] (1) protected Real[1] tank1.portsData_height = tank1.portsData.height
(111)     [ALGB] (2) final Real[2] pipe3.flowModel.roughnesses = {pipe3.roughness, pipe3.roughness} (min = {0.0 for $i1 in 1:2})
(112)     [ALGB] (1) Real $FUN_19
(113)     [ALGB] (1) Real pipe1.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(114)     [ALGB] (1) Real $FUN_17
(115)     [ALGB] (1) protected Real[1] pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1])
(116)     [ALGB] (1) Real[1] tank3.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.tank3.heatTransfer.Medium.temperature(tank3.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(117)     [ALGB] (1) Real $FUN_15
(118)     [ALGB] (1) stream Real[1] ambient_fixed.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(119)     [ALGB] (2) final Real[2] pipe1.flowModel.dimensions = {(4.0 * pipe1.crossArea) / pipe1.perimeter, (4.0 * pipe1.crossArea) / pipe1.perimeter}
(120)     [ALGB] (4) input Real[2, 2] pipe2.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {1.0 for $i1 in 1:2}, max = {1e4 for $i1 in 1:2}, nominal = {300.0 for $i1 in 1:2})
(121)     [ALGB] (1) Real $FUN_13
(122)     [ALGB] (1) Real $FUN_12
(123)     [ALGB] (2) final Real[2] pipe3.flowModel.crossAreas = {pipe3.crossArea, pipe3.crossArea}
(124)     [ALGB] (1) Real[1] pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths
(125)     [ALGB] (1) Real $FUN_11
(126)     [ALGB] (1) final input Real[1, 1] tank3.heatTransfer.states.p = {tank3.medium.state.p} (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(127)     [ALGB] (1) Real $FUN_10
(128)     [ALGB] (1) Real tank3.mb_flow
(129)     [DER-] (1) Real $DER.tank1.m
(130)     [ALGB] (1) stream Real valveDiscrete.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(131)     [DISC] (2) Boolean[2] $SEV_39[$i1]
(132)     [ALGB] (1) Real[1] tank3.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank3.crossArea) * 2.0 * tank3.level + tank3.crossArea}
(133)     [DISC] (1) Boolean $SEV_8
(134)     [ALGB] (1) Real[1] pipe1.flowModel.Fs_p
(135)     [ALGB] (1) Real[1] pipe2.flowModel.Fs_fg
(136)     [DISC] (1) Boolean $SEV_6
(137)     [ALGB] (1) Real[1] tank3.heatTransfer.Q_flows
(138)     [DISC] (1) Boolean $SEV_4
(139)     [ALGB] (1) protected Real[1] tank1.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:1})
(140)     [ALGB] (2) Real[2] tank3.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(141)     [ALGB] (3) protected Real[3] tank2.portsData_height = tank2.portsData.height
(142)     [DISC] (2) Boolean[2] $SEV_34[$i1]
(143)     [DISC] (1) Boolean $SEV_1
(144)     [ALGB] (2) Real[2] tank3.ports.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(145)     [ALGB] (1) protected Real pipe2.flowModel.dp_fric_nominal = sum({Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], ((pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]) / 2.0)[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(146)     [ALGB] (1) protected Real[1] tank1.portsData_diameter = tank1.portsData.diameter
(147)     [ALGB] (1) Real[1] tank1.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.tank1.heatTransfer.Medium.temperature(tank1.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(148)     [ALGB] (1) Real tank2.Hb_flow
(149)     [ALGB] (2) protected Real[2] tank3.portsData_height = tank3.portsData.height
(150)     [DISC] (2) Boolean[2] $SEV_40[$i1]
(151)     [DISC] (3) Boolean[3] $SEV_12[$i1]
(152)     [ALGB] (1) stream Real[1] tank3.topPorts.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(153)     [ALGB] (2) protected Real[2] tank3.levelAbovePort
(154)     [ALGB] (1) stream Real valveDiscrete.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(155)     [ALGB] (1) Real[1] pipe1.flowModel.Is
(156)     [ALGB] (4) input Real[2, 2] pipe2.flowModel.states.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(157)     [ALGB] (1) Real[1] pipe2.flowModel.Is
(158)     [ALGB] (1) Real[1] pipe2.flowModel.dps_fg (start = {pipe2.flowModel.p_a_start - pipe2.flowModel.p_b_start for $i1 in 1:1})
(159)     [ALGB] (1) Real[1] pipe3.flowModel.Is
(160)     [ALGB] (1) final input Real[1, 1] tank3.heatTransfer.states.T = {tank3.medium.state.T} (start = {288.15 for $i1 in 1:1}, min = {1.0 for $i1 in 1:1}, max = {1e4 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(161)     [DISC] (2) protected Boolean[2] tank3.aboveLevel
(162)     [ALGB] (1) Real[1] pipe1.flowModel.dps_fg (start = {pipe1.flowModel.p_a_start - pipe1.flowModel.p_b_start for $i1 in 1:1})
(163)     [ALGB] (1) protected Real[1] tank1.bottomArea
(164)     [ALGB] (1) final Real[1] pipe3.flowModel.pathLengths = {pipe3.length}
(165)     [ALGB] (2) Real[2] pipe1.flowModel.rhos = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(166)     [ALGB] (1) Real[1] ambient_fixed.ports.p (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(167)     [DISC] (1) Boolean $SEV_56
(168)     [DISC] (1) Boolean $SEV_55
(169)     [ALGB] (2) final Real[2] pipe2.flowModel.crossAreas = {pipe2.crossArea, pipe2.crossArea}
(170)     [DISC] (1) Boolean $SEV_54
(171)     [ALGB] (1) Real valveDiscrete.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(172)     [ALGB] (1) stream Real pipe2.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(173)     [DISC] (1) Boolean $SEV_53
(174)     [ALGB] (1) Real tank1.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(175)     [DISC] (1) Boolean $SEV_52
(176)     [DER-] (1) Real $DER.tank2.U
(177)     [ALGB] (1) stream Real pipe3.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(178)     [ALGB] (1) Real tank1.Qb_flow
(179)     [ALGB] (4) input Real[2, 2] pipe1.flowModel.states.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(180)     [ALGB] (1) Real tank3.Hb_flow
(181)     [ALGB] (1) Real pipe1.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(182)     [ALGB] (1) final Real[1] pipe3.flowModel.dheights = {pipe3.height_ab}
(183)     [ALGB] (2) final Real[2] pipe1.flowModel.crossAreas = {pipe1.crossArea, pipe1.crossArea}
(184)     [ALGB] (1) stream Real pipe2.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(185)     [ALGB] (1) flow Real pipe2.port_b.m_flow (min = -1e5, max = 1e60)
(186)     [DISC] (2) Boolean[2] $SEV_38[$i1]
(187)     [ALGB] (1) Real[1] tank1.heatTransfer.Q_flows
(188)     [ALGB] (1) stream Real pipe3.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(189)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_fg
(190)     [ALGB] (2) Real[2] pipe3.flowModel.rhos = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.flowModel.Medium.density(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(191)     [ALGB] (2) final Real[2] pipe1.flowModel.roughnesses = {pipe1.roughness, pipe1.roughness} (min = {0.0 for $i1 in 1:2})
(192)     [DER-] (1) Real $DER.tank2.m
(193)     [ALGB] (1) Real tank1.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(194)     [ALGB] (1) Real[1] tank3.H_flow_top (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(195)     [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60)
(196)     [ALGB] (1) protected Real[1] tank1.levelAbovePort
(197)     [ALGB] (1) flow Real pipe3.port_b.m_flow (min = -1e5, max = 1e60)
(198)     [DISC] (1) Boolean $SEV_45
(199)     [ALGB] (1) Real[1] tank1.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(200)     [DISC] (1) Boolean $SEV_44
(201)     [DISC] (1) Boolean $SEV_43
(202)     [DISC] (1) Boolean $SEV_42
(203)     [DISC] (1) Boolean $SEV_41
(204)     [DISC] (3) Boolean[3] $SEV_11[$i1]
(205)     [ALGB] (1) Real[1] tank2.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.tank2.heatTransfer.Medium.temperature(tank2.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(206)     [ALGB] (4) input Real[2, 2] pipe1.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {1.0 for $i1 in 1:2}, max = {1e4 for $i1 in 1:2}, nominal = {300.0 for $i1 in 1:2})
(207)     [ALGB] (1) Real[1] tank3.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(208)     [ALGB] (1) Real[1] pipe3.flowModel.rhos_act (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {1.0 for $i1 in 1:1})
(209)     [ALGB] (2) Real[2] pipe1.flowModel.vs = {(-pipe1.port_b.m_flow) / (pipe1.flowModel.crossAreas[1] * Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.Medium.density(pipe1.flowModel.states[1])), -pipe1.port_b.m_flow / (Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.Medium.density(pipe1.flowModel.states[2]) * pipe1.flowModel.crossAreas[2])} / pipe1.nParallel
(210)     [ALGB] (1) Real tank2.Qb_flow
(211)     [ALGB] (1) flow Real[1] tank1.heatTransfer.heatPorts.Q_flow
(212)     [ALGB] (1) protected Real[1] tank1.zetas_out
(213)     [ALGB] (2) Real[2] pipe2.flowModel.vs = {(-pipe2.port_b.m_flow) / (pipe2.flowModel.crossAreas[1] * Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.Medium.density(pipe2.flowModel.states[1])), -pipe2.port_b.m_flow / (Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.Medium.density(pipe2.flowModel.states[2]) * pipe2.flowModel.crossAreas[2])} / pipe2.nParallel
(214)     [ALGB] (2) Real[2] pipe3.flowModel.vs = {(-pipe3.port_b.m_flow) / (pipe3.flowModel.crossAreas[1] * Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.Medium.density(pipe3.flowModel.states[1])), -pipe3.port_b.m_flow / (Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.Medium.density(pipe3.flowModel.states[2]) * pipe3.flowModel.crossAreas[2])} / pipe3.nParallel
(215)     [ALGB] (1) Real[1] tank3.topPorts.p (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(216)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_p
(217)     [ALGB] (1) Real valveDiscrete.port_a_T = Modelica.Fluid.Utilities.regStep(995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.temperature(valveDiscrete.state_a), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.temperature(Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.setState_phX(valveDiscrete.port_a.p, valveDiscrete.port_a.h_outflow, {})), valveDiscrete.m_flow_small) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(218)     [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum({Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], ((pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]) / 2.0)[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(219)     [ALGB] (1) Real pipe2.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(220)     [DISC] (2) Boolean[2] $SEV_2[$i1]
(221)     [ALGB] (3) flow Real[3] tank2.ports.m_flow (start = {0.0 for $i1 in 1:3}, min = {-1e5 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3})
(222)     [ALGB] (1) flow Real[1] tank1.ports.m_flow (start = {0.0 for $i1 in 1:1}, min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(223)     [ALGB] (2) flow Real[2] tank3.ports.m_flow (start = {0.0 for $i1 in 1:2}, min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(224)     [ALGB] (2) stream Real[2] tank3.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(225)     [ALGB] (1) protected Real[1] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1])
(226)     [ALGB] (1) Real[1] pipe2.flowModel.Res_turbulent_internal = pipe2.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(227)     [ALGB] (1) Real[1] pipe1.flowModel.Ib_flows
(228)     [ALGB] (2) final Real[2] pipe2.flowModel.dimensions = {(4.0 * pipe2.crossArea) / pipe2.perimeter, (4.0 * pipe2.crossArea) / pipe2.perimeter}
(229)     [ALGB] (1) Real valveDiscrete.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(230)     [ALGB] (3) protected Real[3] tank2.zetas_out
(231)     [DER-] (1) Real $DER.tank3.U
(232)     [ALGB] (1) final Real[1] pipe1.flowModel.pathLengths = {pipe1.length}
(233)     [ALGB] (1) flow Real[1] ambient_fixed.ports.m_flow (min = {-1e60}, max = {1e60})
(234)     [DISC] (3) protected Boolean[3] tank2.aboveLevel
(235)     [DISC] (1) Boolean $SEV_30
(236)     [ALGB] (1) Real[1] tank2.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank2.crossArea) * 2.0 * tank2.level + tank2.crossArea}
(237)     [ALGB] (1) final Real[1] pipe2.flowModel.dheights = {pipe2.height_ab}
(238)     [ALGB] (1) protected Real[1] pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1])
(239)     [DISC] (2) Boolean[2] $SEV_37[$i1]
(240)     [ALGB] (1) protected Real[1] tank1.portsData_height2
(241)     [ALGB] (1) final Real tank2.fluidVolume = tank2.fluidVolume
(242)     [ALGB] (1) Real tank3.Qb_flow
(243)     [ALGB] (1) protected Real pipe3.flowModel.dp_fric_nominal = sum({Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], ((pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]) / 2.0)[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(244)     [ALGB] (2) protected Real[2] tank3.zetas_out
(245)     [DISC] (3) Boolean[3] $SEV_15[$i1]
(246)     [ALGB] (1) Real tank1.level (start = tank1.level_start, StateSelect = prefer)
(247)     [ALGB] (1) Real valveDiscrete.V_flow = (995.586 * valveDiscrete.V_flow) / Modelica.Fluid.Utilities.regStep(995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.density(valveDiscrete.state_a), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.valveDiscrete.Medium.density(valveDiscrete.state_b), valveDiscrete.m_flow_small)
(248)     [DER-] (1) Real $DER.tank3.m
(249)     [ALGB] (1) final Real[1] pipe2.flowModel.pathLengths = {pipe2.length}
(250)     [DISC] (3) Boolean[3] $SEV_10[$i1]
(251)     [ALGB] (2) protected Real[2] tank3.bottomArea
(252)     [ALGB] (1) protected Real valveDiscrete.state_a.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)


System Equations (252/339)
****************************
(1)       [ARRY] (1) tank1.portsData_diameter = tank1.portsData.diameter ($RES_BND_255)
(2)       [ARRY] (1) tank1.portsData_height = tank1.portsData.height ($RES_BND_256)
(3)       [FOR-] (3) ($RES_SIM_81)
(3)       [----] for $i1 in 1:3 loop
(3)       [----]   [SCAL] (1) tank2.bottomArea[$i1] = 3.141592653589793 * (tank2.portsData_diameter2[$i1] / 2.0) ^ 2.0 ($RES_SIM_82)
(3)       [----] end for;
(4)       [ARRY] (1) tank1.heatTransfer.Q_flows = tank1.heatTransfer.heatPorts.Q_flow ($RES_SIM_122)
(5)       [FOR-] (3) ($RES_SIM_83)
(5)       [----] for $i1 in 1:3 loop
(5)       [----]   [SCAL] (1) tank2.ports_emptyPipeHysteresis[$i1] = tank2.portsData_diameter2[$i1] * tank2.hysteresisFactor ($RES_SIM_84)
(5)       [----] end for;
(6)       [ARRY] (1) tank1.heatTransfer.Ts = tank1.heatTransfer.heatPorts.T ($RES_SIM_123)
(7)       [ARRY] (1) tank2.heatTransfer.Q_flows = tank2.heatTransfer.heatPorts.Q_flow ($RES_SIM_87)
(8)       [ARRY] (1) tank2.heatTransfer.Ts = tank2.heatTransfer.heatPorts.T ($RES_SIM_88)
(9)       [SCAL] (1) tank1.medium.state.p = tank1.p_ambient ($RES_SIM_128)
(10)      [SCAL] (1) tank1.medium.state.T = -((-273.15) - tank1.medium.T_degC) ($RES_SIM_129)
(11)      [FOR-] (3) ($RES_EVT_371)
(11)      [----] for $i1 in 1:3 loop
(11)      [----]   [SCAL] (1) $SEV_13[$i1] = tank2.ports[$i1].m_flow >= tank2.m_flow_small ($RES_EVT_372)
(11)      [----] end for;
(12)      [FOR-] (3) ($RES_EVT_373)
(12)      [----] for $i1 in 1:3 loop
(12)      [----]   [SCAL] (1) $SEV_14[$i1] = tank2.ports[$i1].m_flow <= (-tank2.m_flow_small) ($RES_EVT_374)
(12)      [----] end for;
(13)      [FOR-] (3) ($RES_EVT_375)
(13)      [----] for $i1 in 1:3 loop
(13)      [----]   [SCAL] (1) $SEV_15[$i1] = 0.008105694691387022 / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]) >= (0.8105694691387022 * tank2.zetas_out[$i1]) / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]) ($RES_EVT_376)
(13)      [----] end for;
(14)      [SCAL] (1) $SEV_16 = tank2.ports[3].m_flow > 0.0 ($RES_EVT_377)
(15)      [SCAL] (1) $SEV_17 = tank2.ports[2].m_flow > 0.0 ($RES_EVT_378)
(16)      [SCAL] (1) $SEV_18 = tank2.ports[1].m_flow > 0.0 ($RES_EVT_379)
(17)      [ARRY] (1) tank2.heatTransfer.surfaceAreas = {2.0 * $FUN_19 * tank2.level + tank2.crossArea} ($RES_BND_260)
(18)      [ARRY] (1) tank2.heatTransfer.Ts = {tank2.heatTransfer.states.p} ($RES_BND_261)
(19)      [ARRY] (3) tank2.portsData_diameter = tank2.portsData.diameter ($RES_BND_262)
(20)      [SCAL] (1) pipe3.port_b.m_flow + tank2.ports[1].m_flow = 0.0 ($RES_SIM_212)
(21)      [ARRY] (3) tank2.portsData_height = tank2.portsData.height ($RES_BND_263)
(22)      [SCAL] (1) tank3.topPorts[1].m_flow - pipe3.port_b.m_flow = 0.0 ($RES_SIM_213)
(23)      [ARRY] (2) pipe1.flowModel.vs = {-(0.0010044335697769957 * pipe1.port_b.m_flow) / pipe1.flowModel.crossAreas[1], -(0.0010044335697769957 * pipe1.port_b.m_flow) / pipe1.flowModel.crossAreas[2]} / pipe1.nParallel ($RES_BND_264)
(24)      [SCAL] (1) pipe2.port_b.m_flow + tank2.ports[2].m_flow = 0.0 ($RES_SIM_214)
(25)      [ARRY] (2) pipe1.flowModel.crossAreas = {pipe1.crossArea, pipe1.crossArea} ($RES_BND_265)
(26)      [SCAL] (1) tank3.ports[2].m_flow - pipe2.port_b.m_flow = 0.0 ($RES_SIM_215)
(27)      [ARRY] (2) pipe1.flowModel.dimensions = {(4.0 * pipe1.crossArea) / pipe1.perimeter, (4.0 * pipe1.crossArea) / pipe1.perimeter} ($RES_BND_266)
(28)      [SCAL] (1) pipe1.port_b.m_flow + tank1.ports[1].m_flow = 0.0 ($RES_SIM_216)
(29)      [SCAL] (1) pipe3.port_a.h_outflow = tank2.ports[1].h_outflow + system.g * pipe3.height_ab ($RES_SIM_18)
(30)      [ARRY] (2) pipe1.flowModel.roughnesses = {pipe1.roughness, pipe1.roughness} ($RES_BND_267)
(31)      [SCAL] (1) tank2.ports[3].m_flow - pipe1.port_b.m_flow = 0.0 ($RES_SIM_217)
(32)      [SCAL] (1) pipe3.port_b.h_outflow = tank3.topPorts[1].h_outflow - system.g * pipe3.height_ab ($RES_SIM_19)
(33)      [ARRY] (1) pipe1.flowModel.dheights = {pipe1.height_ab} ($RES_BND_268)
(34)      [SCAL] (1) tank2.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_218)
(35)      [SCAL] (1) tank2.medium.state.p = tank2.p_ambient ($RES_SIM_93)
(36)      [ARRY] (1) pipe1.flowModel.pathLengths = {pipe1.length} ($RES_BND_269)
(37)      [SCAL] (1) tank1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_219)
(38)      [SCAL] (1) tank2.medium.state.T = -((-273.15) - tank2.medium.T_degC) ($RES_SIM_94)
(39)      [SCAL] (1) $DER.tank3.m = tank3.mb_flow ($RES_SIM_136)
(40)      [SCAL] (1) $DER.tank3.U = tank3.Qb_flow + tank3.Hb_flow ($RES_SIM_137)
(41)      [SCAL] (1) tank3.U = tank3.m * (4184.0 * ((-273.15) - ((-273.15) - tank3.medium.T_degC))) ($RES_SIM_138)
(42)      [SCAL] (1) tank3.m = 995.586 * tank3.fluidVolume ($RES_SIM_139)
(43)      [SCAL] (1) $SEV_19 = tank2.m >= 0.0 ($RES_EVT_380)
(44)      [SCAL] (1) $SEV_20 = tank2.level <= tank2.height ($RES_EVT_381)
(45)      [SCAL] (1) $SEV_24 = tank1.level >= (tank1.portsData_height2[1] + tank1.ports_emptyPipeHysteresis[1]) or $PRE.tank1.aboveLevel[1] and tank1.level >= (tank1.portsData_height2[1] - tank1.ports_emptyPipeHysteresis[1]) ($RES_EVT_385)
(46)      [SCAL] (1) $SEV_25 = tank1.ports[1].m_flow >= tank1.m_flow_small ($RES_EVT_386)
(47)      [SCAL] (1) $SEV_26 = tank1.ports[1].m_flow <= (-tank1.m_flow_small) ($RES_EVT_387)
(48)      [SCAL] (1) $SEV_27 = 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) >= (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) ($RES_EVT_388)
(49)      [SCAL] (1) $SEV_28 = tank1.ports[1].m_flow > 0.0 ($RES_EVT_389)
(50)      [SCAL] (1) -pipe3.port_b.m_flow = pipe3.flowModel.m_flows[1] ($RES_SIM_21)
(51)      [FOR-] (2) ($RES_BND_270)
(51)      [----] for $i1 in 1:2 loop
(51)      [----]   [SCAL] (1) pipe1.flowModel.rhos[$i1] = 995.586 ($RES_BND_271)
(51)      [----] end for;
(52)      [SCAL] (1) tank3.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_220)
(53)      [ARRY] (1) {0.0} = pipe3.flowModel.Ib_flows - (pipe3.flowModel.Fs_fg + pipe3.flowModel.Fs_p) ($RES_SIM_22)
(54)      [SCAL] (1) tank3.ports[1].m_flow - 995.586 * valveDiscrete.V_flow = 0.0 ($RES_SIM_221)
(55)      [ARRY] (1) pipe3.flowModel.Is = {pipe3.flowModel.m_flows[1] * pipe3.flowModel.pathLengths[1]} ($RES_SIM_23)
(56)      [FOR-] (2) ($RES_BND_272)
(56)      [----] for $i1 in 1:2 loop
(56)      [----]   [SCAL] (1) pipe1.flowModel.mus[$i1] = 0.001 ($RES_BND_273)
(56)      [----] end for;
(57)      [SCAL] (1) pipe2.port_b.p = tank2.ports[2].p ($RES_SIM_222)
(58)      [ARRY] (1) pipe3.flowModel.dps_fg = {(2.0 * (pipe3.flowModel.Fs_fg[1] / pipe3.flowModel.nParallel)) / (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2])} ($RES_SIM_24)
(59)      [SCAL] (1) pipe1.port_a.p = tank2.ports[3].p ($RES_SIM_223)
(60)      [ARRY] (1) pipe3.flowModel.Fs_p = pipe3.flowModel.nParallel * {0.5 * (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2]) * (pipe3.flowModel.states.T - pipe3.flowModel.states.T)} ($RES_SIM_25)
(61)      [ARRY] (1) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_274)
(62)      [SCAL] (1) pipe3.port_b.p = tank2.ports[1].p ($RES_SIM_224)
(63)      [ARRY] (1) pipe3.flowModel.Ib_flows = {0.0} ($RES_SIM_26)
(64)      [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[1] = pipe1.flowModel.Re_turbulent ($RES_BND_275)
(65)      [SCAL] (1) pipe3.port_a.p = tank3.topPorts[1].p ($RES_SIM_225)
(66)      [SCAL] (1) pipe3.flowModel.rhos_act[1] = noEvent(if $SEV_4 then pipe3.flowModel.rhos[1] else pipe3.flowModel.rhos[2]) ($RES_SIM_27)
(67)      [FOR-] (2) ($RES_SIM_140)
(67)      [----] for $i1 in 1:2 loop
(67)      [----]   [SCAL] (1) tank3.aboveLevel[$i1] = $SEV_37[$i1] ($RES_SIM_141)
(67)      [----] end for;
(68)      [ARRY] (1) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1]) ($RES_BND_276)
(69)      [SCAL] (1) pipe2.port_a.p = tank3.ports[2].p ($RES_SIM_226)
(70)      [SCAL] (1) pipe3.flowModel.mus_act[1] = noEvent(if $SEV_4 then pipe3.flowModel.mus[1] else pipe3.flowModel.mus[2]) ($RES_SIM_28)
(71)      [SCAL] (1) pipe1.port_b.p = tank1.ports[1].p ($RES_SIM_227)
(72)      [ARRY] (1) pipe3.flowModel.m_flows = {homotopy(({$FUN_12} .* pipe3.flowModel.nParallel)[1], (pipe3.flowModel.m_flow_nominal / pipe3.flowModel.dp_nominal * (pipe3.flowModel.dps_fg - (pipe3.flowModel.g * pipe3.flowModel.dheights) .* pipe3.flowModel.rho_nominal))[1])} ($RES_SIM_29)
(73)      [FOR-] (2) ($RES_SIM_142)
(73)      [----] for $i1 in 1:2 loop
(73)      [----]   [SCAL] (1) tank3.levelAbovePort[$i1] = if tank3.aboveLevel[$i1] then tank3.level - tank3.portsData_height2[$i1] else 0.0 ($RES_SIM_143)
(73)      [----] end for;
(74)      [ARRY] (2) pipe2.flowModel.vs = {-(0.0010044335697769957 * pipe2.port_b.m_flow) / pipe2.flowModel.crossAreas[1], -(0.0010044335697769957 * pipe2.port_b.m_flow) / pipe2.flowModel.crossAreas[2]} / pipe2.nParallel ($RES_BND_278)
(75)      [SCAL] (1) valveDiscrete.port_b.p = tank3.ports[1].p ($RES_SIM_228)
(76)      [ARRY] (2) pipe2.flowModel.crossAreas = {pipe2.crossArea, pipe2.crossArea} ($RES_BND_279)
(77)      [FOR-] (2) ($RES_SIM_144)
(77)      [----] for $i1 in 1:2 loop
(77)      [----]   [SCAL] (1) tank3.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank3.medium.T_degC)) ($RES_SIM_145)
(77)      [----] end for;
(78)      [FOR-] (2) ($RES_SIM_146)
(78)      [----] for $i1 in 1:2 loop
(78)      [----]   [SCAL] (1) tank3.zetas_out[$i1] = 1.0 + (if tank3.aboveLevel[$i1] then 0.0 else tank3.zetaLarge) ($RES_SIM_147)
(78)      [----] end for;
(79)      [FOR-] (2) ($RES_SIM_148)
(79)      [----] for $i1 in 1:2 loop
(79)      [----]   [SCAL] (1) tank3.ports[$i1].p = system.g * tank3.levelAbovePort[$i1] * 995.586 + tank3.p_ambient + smooth(2, if $SEV_38[$i1] then (0.008105694691387022 * tank3.ports[$i1].m_flow ^ 2.0) / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]) else if $SEV_39[$i1] then -(0.8105694691387022 * tank3.zetas_out[$i1] * tank3.ports[$i1].m_flow ^ 2.0) / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]) else if $SEV_40[$i1] then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank3.ports[$i1].m_flow, tank3.m_flow_small, 0.008105694691387022 / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]), (0.8105694691387022 * tank3.zetas_out[$i1]) / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank3.ports[$i1].m_flow, tank3.m_flow_small, (0.8105694691387022 * tank3.zetas_out[$i1]) / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]), 0.008105694691387022 / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]), false, 1.0)) ($RES_SIM_149)
(79)      [----] end for;
(80)      [SCAL] (1) $SEV_29 = tank1.m >= 0.0 ($RES_EVT_390)
(81)      [SCAL] (1) $SEV_30 = tank1.level <= tank1.height ($RES_EVT_391)
(82)      [FOR-] (2) ($RES_EVT_395)
(82)      [----] for $i1 in 1:2 loop
(82)      [----]   [SCAL] (1) $SEV_34[$i1] = tank3.level >= (tank3.portsData_height2[$i1] + tank3.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_396)
(82)      [----] end for;
(83)      [FOR-] (2) ($RES_EVT_397)
(83)      [----] for $i1 in 1:2 loop
(83)      [----]   [SCAL] (1) $SEV_35[$i1] = tank3.level >= (tank3.portsData_height2[$i1] - tank3.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_398)
(83)      [----] end for;
(84)      [FOR-] (2) ($RES_EVT_399)
(84)      [----] for $i1 in 1:2 loop
(84)      [----]   [SCAL] (1) $SEV_36[$i1] = $TEV_2 and $SEV_35[$i1] ($RES_EVT_400)
(84)      [----] end for;
(85)      [SCAL] (1) pipe2.port_a.h_outflow = tank2.ports[2].h_outflow + system.g * pipe2.height_ab ($RES_SIM_31)
(86)      [ARRY] (2) pipe2.flowModel.dimensions = {(4.0 * pipe2.crossArea) / pipe2.perimeter, (4.0 * pipe2.crossArea) / pipe2.perimeter} ($RES_BND_280)
(87)      [SCAL] (1) 995.586 * valveDiscrete.V_flow + ambient_fixed.ports[1].m_flow = 0.0 ($RES_SIM_230)
(88)      [SCAL] (1) pipe2.port_b.h_outflow = tank3.ports[2].h_outflow - system.g * pipe2.height_ab ($RES_SIM_32)
(89)      [ARRY] (2) pipe2.flowModel.roughnesses = {pipe2.roughness, pipe2.roughness} ($RES_BND_281)
(90)      [SCAL] (1) ambient_fixed.ports[1].p = valveDiscrete.port_a.p ($RES_SIM_231)
(91)      [ARRY] (1) pipe2.flowModel.dheights = {pipe2.height_ab} ($RES_BND_282)
(92)      [ARRY] (3) tank2.portsData_height = tank2.portsData_height2 ($RES_SIM_232)
(93)      [SCAL] (1) -pipe2.port_b.m_flow = pipe2.flowModel.m_flows[1] ($RES_SIM_34)
(94)      [ARRY] (1) pipe2.flowModel.pathLengths = {pipe2.length} ($RES_BND_283)
(95)      [ARRY] (3) tank2.portsData_diameter = tank2.portsData_diameter2 ($RES_SIM_233)
(96)      [ARRY] (1) {0.0} = pipe2.flowModel.Ib_flows - (pipe2.flowModel.Fs_fg + pipe2.flowModel.Fs_p) ($RES_SIM_35)
(97)      [FOR-] (2) ($RES_BND_284)
(97)      [----] for $i1 in 1:2 loop
(97)      [----]   [SCAL] (1) pipe2.flowModel.rhos[$i1] = 995.586 ($RES_BND_285)
(97)      [----] end for;
(98)      [ARRY] (1) tank1.portsData_height = tank1.portsData_height2 ($RES_SIM_234)
(99)      [ARRY] (1) pipe2.flowModel.Is = {pipe2.flowModel.m_flows[1] * pipe2.flowModel.pathLengths[1]} ($RES_SIM_36)
(100)     [ARRY] (1) tank1.portsData_diameter = tank1.portsData_diameter2 ($RES_SIM_235)
(101)     [ARRY] (1) pipe2.flowModel.dps_fg = {(2.0 * (pipe2.flowModel.Fs_fg[1] / pipe2.flowModel.nParallel)) / (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2])} ($RES_SIM_37)
(102)     [FOR-] (2) ($RES_BND_286)
(102)     [----] for $i1 in 1:2 loop
(102)     [----]   [SCAL] (1) pipe2.flowModel.mus[$i1] = 0.001 ($RES_BND_287)
(102)     [----] end for;
(103)     [ARRY] (2) tank3.portsData_height = tank3.portsData_height2 ($RES_SIM_236)
(104)     [ARRY] (1) pipe2.flowModel.Fs_p = pipe2.flowModel.nParallel * {0.5 * (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2]) * (pipe2.flowModel.states.T - pipe2.flowModel.states.T)} ($RES_SIM_38)
(105)     [ARRY] (2) tank3.portsData_diameter = tank3.portsData_diameter2 ($RES_SIM_237)
(106)     [ARRY] (1) pipe2.flowModel.Ib_flows = {0.0} ($RES_SIM_39)
(107)     [SCAL] (1) tank3.port_b_H_flow_bottom[2] = smooth(0, tank3.ports[2].m_flow * (if $SEV_41 then pipe2.port_a.h_outflow else tank3.ports[2].h_outflow)) ($RES_SIM_152)
(108)     [ARRY] (1) pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths ($RES_BND_288)
(109)     [SCAL] (1) tank3.port_b_H_flow_bottom[1] = smooth(0, tank3.ports[1].m_flow * (if $SEV_42 then valveDiscrete.port_b.h_outflow else tank3.ports[1].h_outflow)) ($RES_SIM_153)
(110)     [SCAL] (1) pipe2.flowModel.Res_turbulent_internal[1] = pipe2.flowModel.Re_turbulent ($RES_BND_289)
(111)     [SCAL] (1) tank3.topPorts[1].p = tank3.p_ambient ($RES_SIM_154)
(112)     [SCAL] (1) tank3.topPorts[1].h_outflow = tank3.h_start ($RES_SIM_155)
(113)     [FOR-] (2) ($RES_EVT_401)
(113)     [----] for $i1 in 1:2 loop
(113)     [----]   [SCAL] (1) $SEV_37[$i1] = $SEV_34[$i1] or $SEV_36[$i1] ($RES_EVT_402)
(113)     [----] end for;
(114)     [SCAL] (1) tank3.H_flow_top[1] = smooth(0, tank3.topPorts[1].m_flow * (if $SEV_43 then pipe3.port_a.h_outflow else tank3.topPorts[1].h_outflow)) ($RES_SIM_156)
(115)     [FOR-] (2) ($RES_EVT_403)
(115)     [----] for $i1 in 1:2 loop
(115)     [----]   [SCAL] (1) $SEV_38[$i1] = tank3.ports[$i1].m_flow >= tank3.m_flow_small ($RES_EVT_404)
(115)     [----] end for;
(116)     [SCAL] (1) tank3.Qb_flow = tank3.heatTransfer.Q_flows[1] ($RES_SIM_158)
(117)     [SCAL] (1) tank3.Hb_flow = $FUN_3 + $FUN_4 ($RES_SIM_159)
(118)     [FOR-] (2) ($RES_EVT_405)
(118)     [----] for $i1 in 1:2 loop
(118)     [----]   [SCAL] (1) $SEV_39[$i1] = tank3.ports[$i1].m_flow <= (-tank3.m_flow_small) ($RES_EVT_406)
(118)     [----] end for;
(119)     [FOR-] (2) ($RES_EVT_407)
(119)     [----] for $i1 in 1:2 loop
(119)     [----]   [SCAL] (1) $SEV_40[$i1] = 0.008105694691387022 / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]) >= (0.8105694691387022 * tank3.zetas_out[$i1]) / (995.586 * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1] * tank3.portsData_diameter2[$i1]) ($RES_EVT_408)
(119)     [----] end for;
(120)     [SCAL] (1) $SEV_41 = tank3.ports[2].m_flow > 0.0 ($RES_EVT_409)
(121)     [SCAL] (1) $FUN_1 = sum(tank3.topPorts.m_flow) ($RES_$AUX_332)
(122)     [SCAL] (1) $FUN_2 = sum(tank3.ports.m_flow) ($RES_$AUX_331)
(123)     [SCAL] (1) $FUN_3 = sum(tank3.H_flow_top) ($RES_$AUX_330)
(124)     [SCAL] (1) pipe2.flowModel.rhos_act[1] = noEvent(if $SEV_6 then pipe2.flowModel.rhos[1] else pipe2.flowModel.rhos[2]) ($RES_SIM_40)
(125)     [SCAL] (1) pipe2.flowModel.mus_act[1] = noEvent(if $SEV_6 then pipe2.flowModel.mus[1] else pipe2.flowModel.mus[2]) ($RES_SIM_41)
(126)     [ARRY] (1) pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) ($RES_BND_290)
(127)     [ARRY] (1) pipe2.flowModel.m_flows = {homotopy(({$FUN_11} .* pipe2.flowModel.nParallel)[1], (pipe2.flowModel.m_flow_nominal / pipe2.flowModel.dp_nominal * (pipe2.flowModel.dps_fg - (pipe2.flowModel.g * pipe2.flowModel.dheights) .* pipe2.flowModel.rho_nominal))[1])} ($RES_SIM_42)
(128)     [ARRY] (2) pipe3.flowModel.vs = {-(0.0010044335697769957 * pipe3.port_b.m_flow) / pipe3.flowModel.crossAreas[1], -(0.0010044335697769957 * pipe3.port_b.m_flow) / pipe3.flowModel.crossAreas[2]} / pipe3.nParallel ($RES_BND_292)
(129)     [SCAL] (1) pipe1.port_a.h_outflow = tank1.ports[1].h_outflow + system.g * pipe1.height_ab ($RES_SIM_44)
(130)     [ARRY] (2) pipe3.flowModel.crossAreas = {pipe3.crossArea, pipe3.crossArea} ($RES_BND_293)
(131)     [SCAL] (1) pipe1.port_b.h_outflow = tank2.ports[3].h_outflow - system.g * pipe1.height_ab ($RES_SIM_45)
(132)     [ARRY] (2) pipe3.flowModel.dimensions = {(4.0 * pipe3.crossArea) / pipe3.perimeter, (4.0 * pipe3.crossArea) / pipe3.perimeter} ($RES_BND_294)
(133)     [ARRY] (2) pipe3.flowModel.roughnesses = {pipe3.roughness, pipe3.roughness} ($RES_BND_295)
(134)     [SCAL] (1) -pipe1.port_b.m_flow = pipe1.flowModel.m_flows[1] ($RES_SIM_47)
(135)     [SCAL] (1) tank3.mb_flow = $FUN_1 + $FUN_2 ($RES_SIM_160)
(136)     [ARRY] (1) pipe3.flowModel.dheights = {pipe3.height_ab} ($RES_BND_296)
(137)     [ARRY] (1) {0.0} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_48)
(138)     [SCAL] (1) tank3.fluidVolume = tank3.crossArea * tank3.level + tank3.V0 ($RES_SIM_161)
(139)     [ARRY] (1) pipe3.flowModel.pathLengths = {pipe3.length} ($RES_BND_297)
(140)     [ARRY] (1) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[1] * pipe1.flowModel.pathLengths[1]} ($RES_SIM_49)
(141)     [FOR-] (2) ($RES_BND_298)
(141)     [----] for $i1 in 1:2 loop
(141)     [----]   [SCAL] (1) pipe3.flowModel.rhos[$i1] = 995.586 ($RES_BND_299)
(141)     [----] end for;
(142)     [FOR-] (2) ($RES_SIM_163)
(142)     [----] for $i1 in 1:2 loop
(142)     [----]   [SCAL] (1) tank3.bottomArea[$i1] = 3.141592653589793 * (tank3.portsData_diameter2[$i1] / 2.0) ^ 2.0 ($RES_SIM_164)
(142)     [----] end for;
(143)     [SCAL] (1) $SEV_42 = tank3.ports[1].m_flow > 0.0 ($RES_EVT_410)
(144)     [FOR-] (2) ($RES_SIM_165)
(144)     [----] for $i1 in 1:2 loop
(144)     [----]   [SCAL] (1) tank3.ports_emptyPipeHysteresis[$i1] = tank3.portsData_diameter2[$i1] * tank3.hysteresisFactor ($RES_SIM_166)
(144)     [----] end for;
(145)     [SCAL] (1) $SEV_43 = tank3.topPorts[1].m_flow > 0.0 ($RES_EVT_411)
(146)     [SCAL] (1) $SEV_44 = tank3.m >= 0.0 ($RES_EVT_412)
(147)     [SCAL] (1) $FUN_4 = sum(tank3.port_b_H_flow_bottom) ($RES_$AUX_329)
(148)     [SCAL] (1) $SEV_45 = tank3.level <= tank3.height ($RES_EVT_413)
(149)     [ARRY] (1) tank3.heatTransfer.Q_flows = tank3.heatTransfer.heatPorts.Q_flow ($RES_SIM_169)
(150)     [SCAL] (1) $FUN_6 = sum(tank1.ports.m_flow) ($RES_$AUX_327)
(151)     [SCAL] (1) $FUN_7 = sum(tank1.port_b_H_flow_bottom) ($RES_$AUX_326)
(152)     [SCAL] (1) $FUN_8 = sum(tank2.ports.m_flow) ($RES_$AUX_325)
(153)     [SCAL] (1) $FUN_9 = sum(tank2.port_b_H_flow_bottom) ($RES_$AUX_324)
(154)     [SCAL] (1) $FUN_10 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[1], pipe1.flowModel.rhos[1], pipe1.flowModel.rhos[2], pipe1.flowModel.mus[1], pipe1.flowModel.mus[2], pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (pipe1.flowModel.g * pipe1.flowModel.dheights)[1], (0.5 .* (pipe1.flowModel.crossAreas[1:1] + pipe1.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe1.flowModel.roughnesses[1:1] + pipe1.flowModel.roughnesses[2:2]))[1], pipe1.flowModel.dp_small, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_323)
(155)     [SCAL] (1) $FUN_11 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe2.flowModel.dps_fg[1], pipe2.flowModel.rhos[1], pipe2.flowModel.rhos[2], pipe2.flowModel.mus[1], pipe2.flowModel.mus[2], pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (pipe2.flowModel.g * pipe2.flowModel.dheights)[1], (0.5 .* (pipe2.flowModel.crossAreas[1:1] + pipe2.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe2.flowModel.roughnesses[1:1] + pipe2.flowModel.roughnesses[2:2]))[1], pipe2.flowModel.dp_small, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_322)
(156)     [FOR-] (2) ($RES_BND_300)
(156)     [----] for $i1 in 1:2 loop
(156)     [----]   [SCAL] (1) pipe3.flowModel.mus[$i1] = 0.001 ($RES_BND_301)
(156)     [----] end for;
(157)     [SCAL] (1) $FUN_12 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe3.flowModel.dps_fg[1], pipe3.flowModel.rhos[1], pipe3.flowModel.rhos[2], pipe3.flowModel.mus[1], pipe3.flowModel.mus[2], pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (pipe3.flowModel.g * pipe3.flowModel.dheights)[1], (0.5 .* (pipe3.flowModel.crossAreas[1:1] + pipe3.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe3.flowModel.roughnesses[1:1] + pipe3.flowModel.roughnesses[2:2]))[1], pipe3.flowModel.dp_small, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_321)
(158)     [SCAL] (1) $FUN_13 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (0.5 .* (pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]))[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_320)
(159)     [ARRY] (1) pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths ($RES_BND_302)
(160)     [SCAL] (1) pipe3.flowModel.Res_turbulent_internal[1] = pipe3.flowModel.Re_turbulent ($RES_BND_303)
(161)     [ARRY] (1) pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) ($RES_BND_304)
(162)     [ARRY] (2) tank3.heatTransfer.states = {tank3.medium.state} ($RES_BND_306)
(163)     [ARRY] (2) tank1.heatTransfer.states = {tank1.medium.state} ($RES_BND_307)
(164)     [ARRY] (2) tank2.heatTransfer.states = {tank2.medium.state} ($RES_BND_308)
(165)     [ARRY] (4) pipe1.flowModel.states = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.Medium.ThermodynamicState(pipe1.port_a.p, 273.15 + 2.390057361376673e-4 * tank2.ports[3].h_outflow), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.Medium.ThermodynamicState(pipe1.port_b.p, 273.15 + 2.390057361376673e-4 * tank1.ports[1].h_outflow)} ($RES_BND_309)
(166)     [ARRY] (1) pipe1.flowModel.dps_fg = {(2.0 * (pipe1.flowModel.Fs_fg[1] / pipe1.flowModel.nParallel)) / (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2])} ($RES_SIM_50)
(167)     [SCAL] (1) valveDiscrete.state_a.p = valveDiscrete.port_a.p ($RES_SIM_333)
(168)     [ARRY] (1) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.5 * (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2]) * (pipe1.flowModel.states.T - pipe1.flowModel.states.T)} ($RES_SIM_51)
(169)     [SCAL] (1) valveDiscrete.state_a.T = 273.15 + 2.390057361376673e-4 * ambient_fixed.ports[1].h_outflow ($RES_SIM_334)
(170)     [ARRY] (1) pipe1.flowModel.Ib_flows = {0.0} ($RES_SIM_52)
(171)     [SCAL] (1) valveDiscrete.state_b.p = valveDiscrete.port_b.p ($RES_SIM_335)
(172)     [SCAL] (1) pipe1.flowModel.rhos_act[1] = noEvent(if $SEV_8 then pipe1.flowModel.rhos[1] else pipe1.flowModel.rhos[2]) ($RES_SIM_53)
(173)     [SCAL] (1) valveDiscrete.state_b.T = 273.15 + 2.390057361376673e-4 * tank3.ports[1].h_outflow ($RES_SIM_336)
(174)     [SCAL] (1) pipe1.flowModel.mus_act[1] = noEvent(if $SEV_8 then pipe1.flowModel.mus[1] else pipe1.flowModel.mus[2]) ($RES_SIM_54)
(175)     [ARRY] (1) pipe1.flowModel.m_flows = {homotopy(({$FUN_10} .* pipe1.flowModel.nParallel)[1], (pipe1.flowModel.m_flow_nominal / pipe1.flowModel.dp_nominal * (pipe1.flowModel.dps_fg - (pipe1.flowModel.g * pipe1.flowModel.dheights) .* pipe1.flowModel.rho_nominal))[1])} ($RES_SIM_55)
(176)     [SCAL] (1) $DER.tank2.m = tank2.mb_flow ($RES_SIM_56)
(177)     [SCAL] (1) $DER.tank2.U = tank2.Qb_flow + tank2.Hb_flow ($RES_SIM_57)
(178)     [ARRY] (1) tank3.heatTransfer.Ts = tank3.heatTransfer.heatPorts.T ($RES_SIM_170)
(179)     [SCAL] (1) tank2.U = tank2.m * (4184.0 * ((-273.15) - ((-273.15) - tank2.medium.T_degC))) ($RES_SIM_58)
(180)     [SCAL] (1) tank2.m = 995.586 * tank2.fluidVolume ($RES_SIM_59)
(181)     [SCAL] (1) $SEV_52 = (-995.586 * valveDiscrete.V_flow) > valveDiscrete.m_flow_small ($RES_EVT_420)
(182)     [SCAL] (1) tank3.medium.state.p = tank3.p_ambient ($RES_SIM_175)
(183)     [SCAL] (1) $SEV_53 = (-995.586 * valveDiscrete.V_flow) < (-valveDiscrete.m_flow_small) ($RES_EVT_421)
(184)     [SCAL] (1) tank3.medium.state.T = -((-273.15) - tank3.medium.T_degC) ($RES_SIM_176)
(185)     [SCAL] (1) $SEV_54 = valveDiscrete.m_flow_small > 0.0 ($RES_EVT_422)
(186)     [SCAL] (1) pipe3.flowModel.dp_fric_nominal = sum({$FUN_13}) ($RES_$AUX_319)
(187)     [SCAL] (1) $SEV_55 = 995.586 * valveDiscrete.V_flow > valveDiscrete.m_flow_small ($RES_EVT_423)
(188)     [SCAL] (1) $FUN_15 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (0.5 .* (pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]))[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_318)
(189)     [SCAL] (1) $SEV_56 = 995.586 * valveDiscrete.V_flow < (-valveDiscrete.m_flow_small) ($RES_EVT_424)
(190)     [SCAL] (1) pipe2.flowModel.dp_fric_nominal = sum({$FUN_15}) ($RES_$AUX_317)
(191)     [SCAL] (1) $FUN_17 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (0.5 .* (pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]))[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_316)
(192)     [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum({$FUN_17}) ($RES_$AUX_315)
(193)     [SCAL] (1) $FUN_19 = sqrt(3.141592653589793 * tank2.crossArea) ($RES_$AUX_314)
(194)     [SCAL] (1) $FUN_20 = sqrt(3.141592653589793 * tank1.crossArea) ($RES_$AUX_313)
(195)     [SCAL] (1) $FUN_21 = sqrt(3.141592653589793 * tank3.crossArea) ($RES_$AUX_312)
(196)     [ARRY] (4) pipe2.flowModel.states = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.Medium.ThermodynamicState(pipe2.port_a.p, 273.15 + 2.390057361376673e-4 * tank3.ports[2].h_outflow), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe2.Medium.ThermodynamicState(pipe2.port_b.p, 273.15 + 2.390057361376673e-4 * tank2.ports[2].h_outflow)} ($RES_BND_310)
(197)     [ARRY] (4) pipe3.flowModel.states = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.Medium.ThermodynamicState(pipe3.port_a.p, 273.15 + 2.390057361376673e-4 * tank3.topPorts[1].h_outflow), Modelica.Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2.pipe3.Medium.ThermodynamicState(pipe3.port_b.p, 273.15 + 2.390057361376673e-4 * tank2.ports[1].h_outflow)} ($RES_BND_311)
(198)     [SCAL] (1) $TEV_0 = $PRE.tank2.aboveLevel[$i1] ($RES_EVT_349)
(199)     [FOR-] (3) ($RES_SIM_60)
(199)     [----] for $i1 in 1:3 loop
(199)     [----]   [SCAL] (1) tank2.aboveLevel[$i1] = $SEV_12[$i1] ($RES_SIM_61)
(199)     [----] end for;
(200)     [SCAL] (1) $DER.tank1.m = tank1.mb_flow ($RES_SIM_101)
(201)     [FOR-] (3) ($RES_SIM_62)
(201)     [----] for $i1 in 1:3 loop
(201)     [----]   [SCAL] (1) tank2.levelAbovePort[$i1] = if tank2.aboveLevel[$i1] then tank2.level - tank2.portsData_height2[$i1] else 0.0 ($RES_SIM_63)
(201)     [----] end for;
(202)     [SCAL] (1) $DER.tank1.U = tank1.Qb_flow + tank1.Hb_flow ($RES_SIM_102)
(203)     [SCAL] (1) tank1.U = tank1.m * (4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC))) ($RES_SIM_103)
(204)     [FOR-] (3) ($RES_SIM_64)
(204)     [----] for $i1 in 1:3 loop
(204)     [----]   [SCAL] (1) tank2.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank2.medium.T_degC)) ($RES_SIM_65)
(204)     [----] end for;
(205)     [SCAL] (1) tank1.m = 995.586 * tank1.fluidVolume ($RES_SIM_104)
(206)     [SCAL] (1) tank1.aboveLevel[1] = $SEV_24 ($RES_SIM_105)
(207)     [FOR-] (3) ($RES_SIM_66)
(207)     [----] for $i1 in 1:3 loop
(207)     [----]   [SCAL] (1) tank2.zetas_out[$i1] = 1.0 + (if tank2.aboveLevel[$i1] then 0.0 else tank2.zetaLarge) ($RES_SIM_67)
(207)     [----] end for;
(208)     [SCAL] (1) tank1.levelAbovePort[1] = if tank1.aboveLevel[1] then tank1.level - tank1.portsData_height2[1] else 0.0 ($RES_SIM_106)
(209)     [SCAL] (1) tank1.ports[1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC)) ($RES_SIM_107)
(210)     [FOR-] (3) ($RES_SIM_68)
(210)     [----] for $i1 in 1:3 loop
(210)     [----]   [SCAL] (1) tank2.ports[$i1].p = system.g * tank2.levelAbovePort[$i1] * 995.586 + tank2.p_ambient + smooth(2, if $SEV_13[$i1] then (0.008105694691387022 * tank2.ports[$i1].m_flow ^ 2.0) / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]) else if $SEV_14[$i1] then -(0.8105694691387022 * tank2.zetas_out[$i1] * tank2.ports[$i1].m_flow ^ 2.0) / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]) else if $SEV_15[$i1] then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank2.ports[$i1].m_flow, tank2.m_flow_small, 0.008105694691387022 / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]), (0.8105694691387022 * tank2.zetas_out[$i1]) / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank2.ports[$i1].m_flow, tank2.m_flow_small, (0.8105694691387022 * tank2.zetas_out[$i1]) / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]), 0.008105694691387022 / (995.586 * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1] * tank2.portsData_diameter2[$i1]), false, 1.0)) ($RES_SIM_69)
(210)     [----] end for;
(211)     [SCAL] (1) tank1.zetas_out[1] = 1.0 + (if tank1.aboveLevel[1] then 0.0 else tank1.zetaLarge) ($RES_SIM_108)
(212)     [SCAL] (1) tank1.ports[1].p = 995.586 * system.g * tank1.levelAbovePort[1] + tank1.p_ambient + smooth(2, if $SEV_25 then (8.14163185439231e-6 * tank1.ports[1].m_flow ^ 2.0) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) else if $SEV_26 then -(8.141631854392309e-4 * tank1.zetas_out[1] * tank1.ports[1].m_flow ^ 2.0) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) else if $SEV_27 then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank1.ports[1].m_flow, tank1.m_flow_small, 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank1.ports[1].m_flow, tank1.m_flow_small, (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), false, 1.0)) ($RES_SIM_109)
(213)     [SCAL] (1) valveDiscrete.dp = valveDiscrete.port_a.p - valveDiscrete.port_b.p ($RES_SIM_186)
(214)     [SCAL] (1) valveDiscrete.port_b.h_outflow = ambient_fixed.ports[1].h_outflow ($RES_SIM_189)
(215)     [SCAL] (1) $TEV_1 = $PRE.tank1.aboveLevel ($RES_EVT_350)
(216)     [SCAL] (1) $TEV_2 = $PRE.tank3.aboveLevel[$i1] ($RES_EVT_351)
(217)     [FOR-] (3) ($RES_EVT_352)
(217)     [----] for $i1 in 1:3 loop
(217)     [----]   [SCAL] (1) $SEV_0[$i1] = tank2.level_start >= tank2.portsData_height2[$i1] ($RES_EVT_353)
(217)     [----] end for;
(218)     [SCAL] (1) $SEV_1 = tank1.level_start >= tank1.portsData_height2[1] ($RES_EVT_354)
(219)     [FOR-] (2) ($RES_EVT_355)
(219)     [----] for $i1 in 1:2 loop
(219)     [----]   [SCAL] (1) $SEV_2[$i1] = tank3.level_start >= tank3.portsData_height2[$i1] ($RES_EVT_356)
(219)     [----] end for;
(220)     [SCAL] (1) $SEV_4 = pipe3.flowModel.m_flows[1] > 0.0 ($RES_EVT_358)
(221)     [SCAL] (1) valveDiscrete.port_a_T = smooth(1, if $SEV_55 then valveDiscrete.state_a.T else if $SEV_56 then 273.15 + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow else if $SEV_54 then 0.25 * ((273.15 + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow) - valveDiscrete.state_a.T) * ((-3.0) + (995.586 * valveDiscrete.V_flow / valveDiscrete.m_flow_small) ^ 2.0) * ((995.586 * valveDiscrete.V_flow) / valveDiscrete.m_flow_small) + 0.5 * (273.15 + valveDiscrete.state_a.T + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow) else 0.5 * (273.15 + valveDiscrete.state_a.T + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow)) ($RES_BND_241)
(222)     [SCAL] (1) valveDiscrete.port_b_T = smooth(1, if $SEV_52 then valveDiscrete.state_b.T else if $SEV_53 then 273.15 + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow else if $SEV_54 then 0.5 * (273.15 + valveDiscrete.state_b.T + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow) - 0.25 * ((273.15 + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow) - valveDiscrete.state_b.T) * ((-3.0) + (995.586 * valveDiscrete.V_flow / (-valveDiscrete.m_flow_small)) ^ 2.0) * ((995.586 * valveDiscrete.V_flow) / valveDiscrete.m_flow_small) else 0.5 * (273.15 + valveDiscrete.state_b.T + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow)) ($RES_BND_242)
(223)     [ARRY] (1) tank3.heatTransfer.surfaceAreas = {2.0 * $FUN_21 * tank3.level + tank3.crossArea} ($RES_BND_246)
(224)     [SCAL] (1) tank1.port_b_H_flow_bottom[1] = smooth(0, tank1.ports[1].m_flow * (if $SEV_28 then pipe1.port_b.h_outflow else tank1.ports[1].h_outflow)) ($RES_SIM_111)
(225)     [ARRY] (1) tank3.heatTransfer.Ts = {tank3.heatTransfer.states.p} ($RES_BND_247)
(226)     [SCAL] (1) tank2.port_b_H_flow_bottom[3] = smooth(0, tank2.ports[3].m_flow * (if $SEV_16 then pipe1.port_a.h_outflow else tank2.ports[3].h_outflow)) ($RES_SIM_72)
(227)     [ARRY] (2) tank3.portsData_diameter = tank3.portsData.diameter ($RES_BND_248)
(228)     [SCAL] (1) tank2.port_b_H_flow_bottom[2] = smooth(0, tank2.ports[2].m_flow * (if $SEV_17 then pipe2.port_b.h_outflow else tank2.ports[2].h_outflow)) ($RES_SIM_73)
(229)     [SCAL] (1) tank1.Qb_flow = tank1.heatTransfer.Q_flows[1] ($RES_SIM_113)
(230)     [ARRY] (2) tank3.portsData_height = tank3.portsData.height ($RES_BND_249)
(231)     [SCAL] (1) tank2.port_b_H_flow_bottom[1] = smooth(0, tank2.ports[1].m_flow * (if $SEV_18 then pipe3.port_b.h_outflow else tank2.ports[1].h_outflow)) ($RES_SIM_74)
(232)     [SCAL] (1) tank1.Hb_flow = $FUN_7 ($RES_SIM_114)
(233)     [SCAL] (1) tank1.mb_flow = $FUN_6 ($RES_SIM_115)
(234)     [SCAL] (1) tank2.Qb_flow = tank2.heatTransfer.Q_flows[1] ($RES_SIM_76)
(235)     [SCAL] (1) tank1.fluidVolume = tank1.crossArea * tank1.level + tank1.V0 ($RES_SIM_116)
(236)     [SCAL] (1) tank2.Hb_flow = $FUN_9 ($RES_SIM_77)
(237)     [SCAL] (1) valveDiscrete.port_a.h_outflow = tank3.ports[1].h_outflow ($RES_SIM_190)
(238)     [SCAL] (1) tank2.mb_flow = $FUN_8 ($RES_SIM_78)
(239)     [SCAL] (1) 995.586 * valveDiscrete.V_flow = if open.k then valveDiscrete.k * valveDiscrete.dp else valveDiscrete.k * valveDiscrete.opening_min * valveDiscrete.dp ($RES_SIM_191)
(240)     [SCAL] (1) tank1.bottomArea[1] = 3.141592653589793 * (tank1.portsData_diameter2[1] / 2.0) ^ 2.0 ($RES_SIM_118)
(241)     [SCAL] (1) tank2.fluidVolume = tank2.crossArea * tank2.level + tank2.V0 ($RES_SIM_79)
(242)     [SCAL] (1) ambient_fixed.ports[1].p = ambient_fixed.p ($RES_SIM_192)
(243)     [SCAL] (1) tank1.ports_emptyPipeHysteresis[1] = tank1.portsData_diameter2[1] * tank1.hysteresisFactor ($RES_SIM_119)
(244)     [SCAL] (1) ambient_fixed.ports[1].h_outflow = 4184.0 * ((-273.15) + ambient_fixed.T) ($RES_SIM_193)
(245)     [SCAL] (1) $SEV_6 = pipe2.flowModel.m_flows[1] > 0.0 ($RES_EVT_360)
(246)     [SCAL] (1) $SEV_8 = pipe1.flowModel.m_flows[1] > 0.0 ($RES_EVT_362)
(247)     [FOR-] (3) ($RES_EVT_363)
(247)     [----] for $i1 in 1:3 loop
(247)     [----]   [SCAL] (1) $SEV_9[$i1] = tank2.level >= (tank2.portsData_height2[$i1] + tank2.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_364)
(247)     [----] end for;
(248)     [FOR-] (3) ($RES_EVT_365)
(248)     [----] for $i1 in 1:3 loop
(248)     [----]   [SCAL] (1) $SEV_10[$i1] = tank2.level >= (tank2.portsData_height2[$i1] - tank2.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_366)
(248)     [----] end for;
(249)     [FOR-] (3) ($RES_EVT_367)
(249)     [----] for $i1 in 1:3 loop
(249)     [----]   [SCAL] (1) $SEV_11[$i1] = $TEV_0 and $SEV_10[$i1] ($RES_EVT_368)
(249)     [----] end for;
(250)     [FOR-] (3) ($RES_EVT_369)
(250)     [----] for $i1 in 1:3 loop
(250)     [----]   [SCAL] (1) $SEV_12[$i1] = $SEV_9[$i1] or $SEV_11[$i1] ($RES_EVT_370)
(250)     [----] end for;
(251)     [ARRY] (1) tank1.heatTransfer.surfaceAreas = {2.0 * $FUN_20 * tank1.level + tank1.crossArea} ($RES_BND_253)
(252)     [ARRY] (1) tank1.heatTransfer.Ts = {tank1.heatTransfer.states.p} ($RES_BND_254)